JPS61225592A - Method to improve fluidizing property of two-phase flow utilizing electric field - Google Patents

Method to improve fluidizing property of two-phase flow utilizing electric field

Info

Publication number
JPS61225592A
JPS61225592A JP6742585A JP6742585A JPS61225592A JP S61225592 A JPS61225592 A JP S61225592A JP 6742585 A JP6742585 A JP 6742585A JP 6742585 A JP6742585 A JP 6742585A JP S61225592 A JPS61225592 A JP S61225592A
Authority
JP
Japan
Prior art keywords
pipe
flow
electrode
gas
wire electrode
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP6742585A
Other languages
Japanese (ja)
Other versions
JPH023918B2 (en
Inventor
Akira Yabe
彰 矢部
Takao Takeya
竹谷 隆夫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP6742585A priority Critical patent/JPS61225592A/en
Publication of JPS61225592A publication Critical patent/JPS61225592A/en
Publication of JPH023918B2 publication Critical patent/JPH023918B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/16Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying an electrostatic field to the body of the heat-exchange medium

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

PURPOSE:To obtain a large amount of fluid flow by small electric power, by flowing fluid in the neighborhood of the center of a pipe, by gathering gas in the neighborhood of the inside wall of a pipe, by applying high voltage across a wire electrode and a mesh electrode. CONSTITUTION:A wire electrode 12 is provided on the inside wall of a pipe 1 along the axial direction of a pipe 1, and a mesh electrode 13 is provided surrounding the outer side of a wire electrode 12. The wire electrode 12 is in no contact with the mesh electrode 13. When high voltage is applied across the wire electrode 12 and the mesh electrode 13, a gas 3 is driven out in the direction of a mesh electrode 13, of which electric field is weaker. The gas 3 gathers in the neighborhood of the inside wall 4 of a pipe 1, while a fluid 2 flows through the part in the neighborhood of the center of a pipe 1. With such an arrangement, the heat transferring rate can be increased in both regions of a foamed gas flow and of a ring fluid flow in a boiling heat exchanger. Since a fluid runs through the region in the neighborhood of the center of a pipe out of two-phases flow in the pipe, pressure loss is lowered, and a large amount of flow can be circulated by small electric power.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、電場を利用して管路中の二相流の流動特性を
改善する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method of improving the flow characteristics of two-phase flow in a conduit using an electric field.

(従来技術) 従来、管路内を流れる水、フロン等の液体に対し熱伝達
して沸騰させる熱交換器においては、流れの方向におい
て気泡流、環状流ζ噴霧流、蒸気流となりJこのうち気
泡流、環状流の部分で熱伝達があまり良好でなく、かつ
液体を圧送するための圧力損失が環状流の位置で大きく
液体の流量を気体の流量に合致させんとすることが困難
であるという問題点があった。
(Prior art) Conventionally, in a heat exchanger that transfers heat to a liquid such as water or fluorocarbon flowing in a pipe to boil it, in the direction of flow there are bubble flow, annular flow, spray flow, and vapor flow. Heat transfer is not very good in the bubble flow and annular flow areas, and the pressure loss for pumping the liquid is large at the annular flow position, making it difficult to match the liquid flow rate to the gas flow rate. There was a problem.

この問題点を明らかにするために、第2図において熱交
換器内の管路1を流れる液体の流動特性を示す。管路1
を流れる液体2に管路1外の熱Qが伝達されるため液体
2中に気体3が気泡としてあられれ二相流となる。
In order to clarify this problem, FIG. 2 shows the flow characteristics of the liquid flowing through the pipe line 1 in the heat exchanger. Conduit 1
Since the heat Q from outside the pipe line 1 is transferred to the liquid 2 flowing through the liquid 2, gas 3 forms bubbles in the liquid 2, resulting in a two-phase flow.

この二相流は、流れの始めの方では均一な気泡流である
(A域)、流れにしたがって管路1の中央付近は気体3
が流れ、液体2は管路1の内壁面4付近を環状に流れる
環状流となる(B域)。
This two-phase flow is a uniform bubble flow at the beginning of the flow (region A).
flows, and the liquid 2 becomes an annular flow that flows in an annular manner near the inner wall surface 4 of the pipe line 1 (area B).

次に、液体2が液滴と−なる噴霧流となる(C域)6そ
して最後に、蒸気となる(D域)。
Next, the liquid 2 becomes a spray stream that becomes droplets (zone C)6, and finally it becomes vapor (zone D).

(発明が解決しようとする問題点) 従来の熱交換器の管路1における前記A域では気泡を管
路1の内面壁4付近へ集合させることにより境界層を乱
して熱伝達効率を上げるようにすることが望ましく、前
記B域の環状流に相当する箇所においては液体2と管路
1の内壁面4の摩擦が大きく中央にある気体3が大量に
流れるのに対し液体2の流量が少ないものとなっていた
。すなわち、熱伝達が望ましくないことと液体2を圧送
するための圧力損失が大きいため、蒸気と液体との好ま
しい流れとすることができない問題があった。
(Problems to be Solved by the Invention) In the area A of the conduit 1 of the conventional heat exchanger, air bubbles are gathered near the inner wall 4 of the conduit 1 to disturb the boundary layer and increase heat transfer efficiency. It is desirable that the flow rate of the liquid 2 is large in the part corresponding to the annular flow in the region B, where the friction between the liquid 2 and the inner wall surface 4 of the pipe line 1 is large and the gas 3 in the center flows in large quantities. There were fewer of them. That is, there was a problem in that it was not possible to achieve a desirable flow of vapor and liquid because heat transfer was undesirable and the pressure loss for pumping the liquid 2 was large.

本発明は、上述のA域、B域の流動特性を改善するもの
である。すなわち、本発明の目的は、液体を管路の中央
付近を流れるようにし、気泡を管路の内壁付近に集める
ことによって熱伝達率を向上させ圧力損失を少なくし小
さな動力によって液体の流量を多くする方法を提供する
ことにある。
The present invention improves the flow characteristics in the above-mentioned regions A and B. That is, the purpose of the present invention is to make the liquid flow near the center of the pipe and collect air bubbles near the inner wall of the pipe to improve the heat transfer coefficient, reduce pressure loss, and increase the flow rate of the liquid with a small amount of power. The goal is to provide a way to do so.

(問題点を解決するための手段) 上記目的を達成するために、本発明では次のように二相
流の流動特性を改善している。
(Means for Solving the Problems) In order to achieve the above object, the present invention improves the flow characteristics of two-phase flow as follows.

二相流が流れている管路の中の気泡流及び/或は環状流
の位置に管路の軸方法に沿って線電極を設け、線電極の
外側を囲んでメツシュ電極を設け、前記線電極とメツシ
ュ電極との開に高電圧をかけて、気体を管路の内壁面付
近に集め、管路の中央付近を液体の流れとする。
A wire electrode is provided along the axis of the pipe at the position of the bubble flow and/or annular flow in the pipe through which the two-phase flow is flowing, and a mesh electrode is provided surrounding the outside of the wire electrode, A high voltage is applied between the electrode and the mesh electrode to collect the gas near the inner wall surface of the conduit, creating a liquid flow near the center of the conduit.

なお、本発明は熱交換器の流動特性の改善に限らず、そ
の他液体と気体の二相流一般の流動特性の改善をも包含
する。
Note that the present invention is not limited to improving the flow characteristics of a heat exchanger, but also includes improving the flow characteristics of two-phase flows of liquid and gas in general.

(作用) 本発明は、犬のように作用する。(effect) The invention works like a dog.

線電極とメツシュ電極とに電圧をかけると、線電極の方
がメツシュ電極よりも電界が強いものとなる。液体より
も誘電率が小さい気体の気泡において、電界の強い線電
極と同じ電極の電荷が気液界面に生じる。そのため、気
泡は電界の弱いメツシュ電極の方向にはじき出される。
When a voltage is applied to a wire electrode and a mesh electrode, the electric field of the wire electrode is stronger than that of the mesh electrode. In gas bubbles with a lower dielectric constant than liquid, the same electrode charge as a wire electrode with a strong electric field is generated at the gas-liquid interface. Therefore, the bubbles are expelled in the direction of the mesh electrode where the electric field is weak.

さらに、メツシュ電極と管内壁との間は電界がOである
ため気泡はハシュ電極か焉じ一出され、管内壁とメツシ
ュ電極間に存在する。
Further, since the electric field between the mesh electrode and the inner wall of the tube is O, air bubbles are ejected from the hash electrode and exist between the inner wall of the tube and the mesh electrode.

(実施例) 以下に、本発明の一実施例を第1図及び第2図に基づい
て説明する。本実施例は、熱交換器における液体の流動
特性を改善して小さな動力で足りるようにしたもの関す
る。
(Example) An example of the present invention will be described below based on FIGS. 1 and 2. This embodiment relates to a heat exchanger in which the flow characteristics of liquid are improved so that a small amount of power is required.

第1図は、熱交換器における上述の管路1のA域、B域
に相当する箇所に流動特性改善のための装置11を設置
したものを示している。
FIG. 1 shows a heat exchanger in which a device 11 for improving flow characteristics is installed at locations corresponding to areas A and B of the above-mentioned pipe line 1.

管路1の中に管路1の軸方向に沿って線電極を12設け
、この線電極12の外側を囲んでメツシュ電極13を設
ける。線電極12とメツシュ電極13は非接触状態であ
る。線電極12とメツシュ電極13との開に高電圧をか
ける。14は電源である。
12 wire electrodes are provided in the pipe 1 along the axial direction of the pipe 1, and a mesh electrode 13 is provided surrounding the outside of the wire electrode 12. The wire electrode 12 and the mesh electrode 13 are in a non-contact state. A high voltage is applied across the line electrode 12 and mesh electrode 13. 14 is a power source.

線電極12の電界は、メツシュ電極13の電界よりも強
い。気液界面には、電界の強い線電極12と同じ電荷(
本実施例では正の電荷)が生じ、気体3は電界の弱いメ
ツシュ電極13の方向にはじき出される。こうして、管
路1の内壁面4付近に気体3が集まり、管路1の中央付
近は液体2の流れとなる。
The electric field of the wire electrode 12 is stronger than the electric field of the mesh electrode 13. The gas-liquid interface has the same charge (
In this embodiment, a positive charge is generated, and the gas 3 is expelled in the direction of the mesh electrode 13 where the electric field is weak. In this way, the gas 3 gathers near the inner wall surface 4 of the pipe 1, and the liquid 2 flows near the center of the pipe 1.

液体2が管路1の中央付近を流れるので圧力損失が少な
く、液体2の流量を多くできる。
Since the liquid 2 flows near the center of the pipe line 1, pressure loss is small and the flow rate of the liquid 2 can be increased.

また、気体3がわずかしか生じていない段階において本
実施例を用いて、管路1の内壁面4の境界層15を乱し
より多くの気泡の発生を助けて液体2に対する熱の伝達
量を増大させることも可能である。つまり、本発明に係
る方法を熱交換器に適用すると、管路1を流れる液体の
流量を多くできると共に熱伝達量を向上させることも可
能である。
In addition, by using this embodiment at a stage when only a small amount of gas 3 is generated, the boundary layer 15 on the inner wall surface 4 of the pipe line 1 is disturbed to help generate more bubbles, thereby reducing the amount of heat transferred to the liquid 2. It is also possible to increase it. That is, when the method according to the present invention is applied to a heat exchanger, it is possible to increase the flow rate of liquid flowing through the pipe line 1 and also to improve the amount of heat transfer.

他の実施例として次のものもある。ガソリン等の燃料中
に空気の気泡を混合し熱機関に送り、有害〃スの発生を
防止する技術がある。この二相流でも燃料が管路1の内
壁面に沿って流れ、管路1の中央を空気が流れる環状流
となるおそれがある。環状流となると空気が大量に送ら
れ燃料がわずかしか送られないため燃焼上好ましくない
Other examples include the following. There is a technology that mixes air bubbles into fuel such as gasoline and sends it to a heat engine to prevent the generation of harmful gas. Even in this two-phase flow, the fuel flows along the inner wall surface of the pipe line 1, and there is a risk that an annular flow may occur in which air flows through the center of the pipe line 1. An annular flow is unfavorable for combustion because a large amount of air is sent and only a small amount of fuel is sent.

そこで、燃料と気泡の二相流を第1図に示す装置11と
同じものを用いて気泡を管路1の内壁面4付近に集め、
燃料が管路の中央を流れるようにするのである。これに
よって、燃料と空気を好ましい割合で送ることができる
Therefore, the two-phase flow of fuel and bubbles is carried out using the same device 11 shown in FIG. 1 to collect the bubbles near the inner wall surface 4 of the pipe line 1.
This allows the fuel to flow through the center of the pipe. This allows fuel and air to be delivered in a preferred ratio.

(発明の効果) 本発明によれば、次の効果を奏する。(Effect of the invention) According to the present invention, the following effects are achieved.

沸騰熱交換器における気泡流、環状流の位置で熱伝達を
向上させることができる。
Heat transfer can be improved at the location of bubble flow and annular flow in boiling heat exchangers.

管路中の二相流において液体を管路の中央付近を流すの
で、圧力損失が少なく、多くの流量の液体を小さな動力
で流すことができる。
Since the liquid flows near the center of the pipe in a two-phase flow in the pipe, there is little pressure loss, and a large amount of liquid can be flowed with a small amount of power.

また、二相流を移送する場合において気体だけが大量に
移送されるということをなくすことができる。
Furthermore, when transferring a two-phase flow, it is possible to avoid transferring only a large amount of gas.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、本発明の一実施例を示す縦断面図、第2図は
、第1図のI−1線横断面図、第3図は、従来における
熱交換器の管路な流れる液体の流動特性を示す縦新面図
、 1:管路 2:液体 3:気体 4:内壁面 12:li電極 13:メッシュ電極
FIG. 1 is a longitudinal cross-sectional view showing an embodiment of the present invention, FIG. 2 is a cross-sectional view taken along line I-1 in FIG. Vertical new view showing the flow characteristics of 1: Pipe 2: Liquid 3: Gas 4: Inner wall surface 12: Li electrode 13: Mesh electrode

Claims (1)

【特許請求の範囲】[Claims] 二相流が流れている管路(1)の中の気泡流(A)及び
/或は環状流(B)位置に管路(1)の軸方法に沿って
線電極(12)を設け、線電極(12)の外側を囲んで
メッシュ電極(13)を設け、前記線電極(12)とメ
ッシュ電極(13)との間に高電圧をかけて、気体(3
)を管路(1)の内壁面(4)付近に集め、管路(1)
の中央付近を液体(2)の流れとすることを特徴とする
電場を利用した二相流の流動特性の改善方法。
a wire electrode (12) is provided along the axis of the pipe (1) at the bubble flow (A) and/or annular flow (B) position in the pipe (1) through which the two-phase flow is flowing; A mesh electrode (13) is provided surrounding the outside of the wire electrode (12), and a high voltage is applied between the wire electrode (12) and the mesh electrode (13) to generate the gas (3).
) is collected near the inner wall surface (4) of the pipe (1), and
A method for improving the flow characteristics of a two-phase flow using an electric field, characterized in that a liquid (2) flows near the center of the flow.
JP6742585A 1985-03-29 1985-03-29 Method to improve fluidizing property of two-phase flow utilizing electric field Granted JPS61225592A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6742585A JPS61225592A (en) 1985-03-29 1985-03-29 Method to improve fluidizing property of two-phase flow utilizing electric field

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6742585A JPS61225592A (en) 1985-03-29 1985-03-29 Method to improve fluidizing property of two-phase flow utilizing electric field

Publications (2)

Publication Number Publication Date
JPS61225592A true JPS61225592A (en) 1986-10-07
JPH023918B2 JPH023918B2 (en) 1990-01-25

Family

ID=13344546

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6742585A Granted JPS61225592A (en) 1985-03-29 1985-03-29 Method to improve fluidizing property of two-phase flow utilizing electric field

Country Status (1)

Country Link
JP (1) JPS61225592A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5072780A (en) * 1988-11-18 1991-12-17 Agency Of Industrial Science & Technology, Ministry Of International Trade & Industry Method and apparatus for augmentation of convection heat transfer in liquid
US5769155A (en) * 1996-06-28 1998-06-23 University Of Maryland Electrohydrodynamic enhancement of heat transfer

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5072780A (en) * 1988-11-18 1991-12-17 Agency Of Industrial Science & Technology, Ministry Of International Trade & Industry Method and apparatus for augmentation of convection heat transfer in liquid
US5769155A (en) * 1996-06-28 1998-06-23 University Of Maryland Electrohydrodynamic enhancement of heat transfer

Also Published As

Publication number Publication date
JPH023918B2 (en) 1990-01-25

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